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<dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:invenio="http://invenio-software.org/elements/1.0" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:language>eng</dc:language><dc:creator>Aznar, M.</dc:creator><dc:creator>Manyà, J. J.</dc:creator><dc:creator>García, G.</dc:creator><dc:creator>Sánchez, J.L.</dc:creator><dc:creator>Murillo, M. B.</dc:creator><dc:title>Influence of freeboard temperature, fluidization velocity and particle size on tar production and composition during the air gasification of sewage sludge</dc:title><dc:identifier>ART-2008-60984</dc:identifier><dc:description>The influence of freeboard temperature, fluidization velocity, and particle size on tar production and composition during the air gasification of dried sewage sludge has been researched using a bench-scale gasifier. Of the operating variables analyzed, the results obtained from a statistical analysis (ANOVA and PCA) indicate that only the freeboard temperature has a significant influence on tar production. The results also show that freeboard temperature is the key factor that influences the tar composition. A high freeboard temperature reduces the amount of tar produced, but the tar compounds obtained are mainly PAH, which could require a more complicated secondary treatment for tar removal. Nevertheless, an increase in the freeboard temperature value implies a substantial increase in both low heating value and cold gas efficiency (6.5% and 10.8%, respectively, when the required freeboard temperature was increased from 873 to 1123 K). Future studies should focus on testing/developing catalytic materials able to degrade (in a secondary treatment) tar with a high content of PAH compounds.</dc:description><dc:date>2008</dc:date><dc:source>http://zaguan.unizar.es/record/150414</dc:source><dc:identifier>http://zaguan.unizar.es/record/150414</dc:identifier><dc:identifier>oai:zaguan.unizar.es:150414</dc:identifier><dc:identifier.citation>Energy and Fuels 22, 4 (2008), 2840-2850</dc:identifier.citation><dc:rights>All rights reserved</dc:rights><dc:rights>http://www.europeana.eu/rights/rr-f/</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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